ES2562770T3 - Process for the production of [2- (4-fluoro-benzyl) -phenyl] -acetic acid - Google Patents
Process for the production of [2- (4-fluoro-benzyl) -phenyl] -acetic acid Download PDFInfo
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Abstract
Procedimiento para la producción del ácido [2-(4-fluoro-bencil)-fenil]-acético, que comprende las subsiguientes etapas a) hasta e): a) hacer reaccionar el anhídrido de ácido ftálico con el fluorobenceno en una reacción de Friedel Crafts usando el fluorobenceno propiamente dicho como el disolvente y el cloruro de aluminio como el ácido de Lewis a la temperatura de reflujo, en la que se usa el cloruro de aluminio en una relación molar con respecto al anhídrido de ácido que es >2:1; b) pasando por reducir el producto obtenido en la etapa a) junto al resto de cetona usando hidrógeno gaseoso, opcionalmente en la presencia de un catalizador de Pd/C, y usando el isopropanol (iPrOH) como el disolvente; c) reducir el producto que se ha obtenido en la etapa b) con 2,3 equivalentes del dihidro-bis (2-metoxi-etoxi) aluminato de sodio (Red-Al) para formar el correspondiente alcohol; d) clorar el alcohol obtenido en la etapa c) usando un ácido clorhídrico acuoso como el agente de cloración, a 90 ºC en un recipiente cerrado, y e) insertar CO dentro del producto obtenido en la etapa d) por medio de un apropiado sistema catalítico que contiene Pd, haciendo reaccionar con CO en una mezcla de THF y H2O en la presencia de a) acetato de sodio, K2C03 o Et3N y b) trifenilfosfina.Process for the production of [2-(4-fluoro-benzyl)-phenyl]-acetic acid, comprising the subsequent steps a) to e): a) reacting phthalic acid anhydride with fluorobenzene in a Friedel reaction Crafts using fluorobenzene itself as the solvent and aluminum chloride as the Lewis acid at reflux temperature, where aluminum chloride is used in a molar ratio to acid anhydride that is >2:1 ; b) by reducing the product obtained in step a) together with the ketone moiety using hydrogen gas, optionally in the presence of a Pd/C catalyst, and using isopropanol (iPrOH) as the solvent; c) reducing the product obtained in step b) with 2.3 equivalents of sodium dihydro-bis (2-methoxy-ethoxy) aluminate (Red-Al) to form the corresponding alcohol; d) chlorinating the alcohol obtained in step c) using an aqueous hydrochloric acid as the chlorinating agent, at 90 ºC in a closed container, and e) inserting CO into the product obtained in step d) by means of an appropriate catalytic system containing Pd, by reacting with CO in a mixture of THF and H2O in the presence of a) sodium acetate, K2C03 or Et3N and b) triphenylphosphine.
Description
DESCRIPCIONDESCRIPTION
Procedimiento para la produccion del acido [2-(4-fluoro-bencil)-fenil]-aceticoProcedure for the production of [2- (4-fluoro-benzyl) -phenyl] -acetic acid
El presente invento a un nuevo procedimiento para la produccion del acido [2-(4-fluoro-bencil)-fenil]-acetico, un compuesto que es obtenible a partir del anlmdrido de acido ftalico.The present invention to a new process for the production of [2- (4-fluoro-benzyl) -phenyl] -acetic acid, a compound that is obtainable from the phthalic acid anhydride.
5 Este derivado es un compuesto intermedio importante en la smtesis de una serie de compuestos, que se divulgan en el documento de solicitud de patente internacional WO 97/38991, que tiene la formula general (A) en donde R1 y R1 son inter alia hidrogeno y/o metilo, R3y R4 son hidrogeno o halogeno, X es CH2, O o S, n es 1 yp yq son 0, 1 o 2.This derivative is an important intermediate compound in the synthesis of a series of compounds, which are disclosed in the international patent application document WO 97/38991, which has the general formula (A) wherein R1 and R1 are inter alia hydrogen and / or methyl, R3 and R4 are hydrogen or halogen, X is CH2, O or S, n is 1 and p and q are 0, 1 or 2.
Se encontro que los compuestos de acuerdo con la Formula (A) son utiles para el tratamiento y/o la prevencion de 10 trastornos del sistema nervioso central (CNS), trastornos cardiovasculares y trastornos gastrointestinales. Su smtesis se ha descrito, entre otras referencias, en los documentos WO03/048146y WO03/048147. En estos ultimos documentos (vease el Esquema 1), se ha divulgado que el acido [2-(4-fluoro-bencil)-fenil]-acetico de acuerdo con la Formula (I) se puede preparar por adaptacion de una secuencia de operaciones que es conocida en la especialidad (por el documento de patente francesa n° 4395M, fechado el 10 de Octubre de 1966; Can. J. Chem., 1971,49, 74615 754), comenzando por una reaccion de acilacion segun Friedel-Crafts usando el fluorobenceno y el anhfdrido deThe compounds according to Formula (A) were found to be useful for the treatment and / or prevention of 10 central nervous system (CNS) disorders, cardiovascular disorders and gastrointestinal disorders. Its synthesis has been described, among other references, in WO03 / 048146 and WO03 / 048147. In these last documents (see Scheme 1), it has been disclosed that [2- (4-fluoro-benzyl) -phenyl] -acetic acid according to Formula (I) can be prepared by adapting a sequence of operations which is known in the specialty (by French Patent Document No. 4395M, dated October 10, 1966; Can. J. Chem., 1971,49, 74615 754), beginning with an acylation reaction according to Friedel-Crafts using fluorobenzene and the anhydride of
acido ftalico para formar un ceto-acido de acuerdo con la Formula (IV), seguido por una eliminacion por reduccion del grupo de cetona y una homologacion de la funcion de acido carboxflico.phthalic acid to form a keto-acid according to Formula (IV), followed by a removal by reduction of the ketone group and a homologation of the carboxylic acid function.
Esquema 1Scheme 1
20 El problema que se plantea con este esquema de reaccion consiste en que varias etapa de la smtesis padecen de diversas desventajas: se necesitan unos disolventes desfavorables para el medio ambiente, se consigue un bajo rendimiento y se precisa el uso de unos complejos reaccionantes o la formacion de unas indeseadas mezclas de sales, tales como por ejemplo el Et3NH+Cl\20 The problem that arises with this reaction scheme is that several stages of the synthesis suffer from various disadvantages: environmentally friendly solvents are needed, low performance is achieved and the use of reactant complexes is required or formation of unwanted salt mixtures, such as, for example, Et3NH + Cl \
El objetivo del presente invento es proporcionar un procedimiento para la produccion del acido [2-(4-fluoro-bencil)- 25 fenil]-acetico, que sea apropiado para realizarse en unos reactores a escala industrial (p.ej. que sea mas limpio y mas eficiente).The objective of the present invention is to provide a process for the production of [2- (4-fluoro-benzyl) -25 phenyl] -acetic acid, which is suitable for carrying out in reactors on an industrial scale (eg more clean and more efficient).
Otro objetivo del presente invento es proporcionar un procedimiento en el que el acido [2-(4-fluoro-bencil)-fenil]- acetico se obtenga como un material cristalino con una pureza > 95 %.Another object of the present invention is to provide a process in which the [2- (4-fluoro-benzyl) -phenyl] -acetic acid is obtained as a crystalline material with a purity> 95%.
De manera muy sorprendente, los autores del invento han encontrado que las desventajas de los procedimientos 30 conocidos se pueden superar mediante un procedimiento que comprende las subsiguientes etapas a) hasta e):Very surprisingly, the authors of the invention have found that the disadvantages of the known methods can be overcome by a method comprising the subsequent steps a) to e):
a) hacer reaccionar el anhfdrido de acido ftalico con el fluorobenceno en una reaccion de Friedel Crafts usando el fluorobenceno propiamente dicho como el disolvente y el cloruro de aluminio como el acido de Lewis a la temperatura de reflujo, en la que se usa el cloruro de aluminio en una relacion molar con respecto al anhfdrido de acido que es >2:1;a) reacting the phthalic acid anhydride with the fluorobenzene in a Friedel Crafts reaction using the fluorobenzene itself as the solvent and the aluminum chloride as the Lewis acid at the reflux temperature, in which the chloride of aluminum in a molar ratio with respect to the acid anhydride which is> 2: 1;
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b) pasando por reducir el producto obtenido en la etapa a) junto al resto de cetona usando hidrogeno gaseoso, opcionalmente en la presencia de un catalizador de Pd/C, y usando el isopropanol (iPrOH) como el disolvente;b) by reducing the product obtained in step a) together with the rest of the ketone using hydrogen gas, optionally in the presence of a Pd / C catalyst, and using isopropanol (iPrOH) as the solvent;
c) reducir el producto que se ha obtenido en la etapa b) con 2,3 equivalentes del dihidro-bis (2-metoxi-etoxi) aluminato de sodio (Red-Al) para formar el correspondiente alcohol;c) reduce the product obtained in step b) with 2.3 equivalents of sodium dihydro-bis (2-methoxy-ethoxy) aluminate (Red-Al) to form the corresponding alcohol;
d) clorar el alcohol obtenido en la etapa c) usando un acido clorhfdrico acuoso como el agente de cloracion, a 90 °C en un recipiente cerrado, yd) chlorinate the alcohol obtained in step c) using an aqueous hydrochloric acid as the chlorinating agent, at 90 ° C in a closed container, and
e) insertar CO dentro del producto obtenido en la etapa d) por medio de un apropiado sistema catalftico que contiene Pd, haciendo reaccionar con CO en una mezcla de THF (tetrahidrofurano) y agua en la presencia de a) acetato de sodio, K2C03 o Et3N y b) trifenilfosfina.e) insert CO into the product obtained in step d) by means of an appropriate catalytic system containing Pd, reacting with CO in a mixture of THF (tetrahydrofuran) and water in the presence of a) sodium acetate, K2C03 or Et3N and b) triphenylphosphine.
Una similar etapa e) de la reaccion por sf misma se describe en el documento de solicitud de patente europea EP 1 207 148 A1 (Clariant GmbH, 22 de Mayo de 2002).A similar step e) of the reaction itself is described in European patent application document EP 1 207 148 A1 (Clariant GmbH, May 22, 2002).
El procedimiento de acuerdo con el invento se puede describir esquematicamente de la siguiente manera (vease el Esquema 2):The process according to the invention can be described schematically as follows (see Scheme 2):
Esquema 2Scheme 2
En la etapa a) se usa una reaccion de Friedel Crafts usando el clorobenceno propiamente dicho como el disolvente y cloruro de aluminio como el acido de Lewis para la reaccion de Friedel-Crafts. El cloruro de aluminio se usa en una relacion molar con respecto al anhfdrido de acido ftalico que es > 2:1. El uso de menos cantidad del cloruro de aluminio conduce a una conversion incompleta. Preferentemente, en la etapa a), la reaccion se realiza a la temperatura de reflujo del fluorobenceno, que es de 75-80 °C. Cuando la reaccion se realiza a una temperatura mas baja, disminuye la velocidad de reaccion. Preferentemente, la mezcla de reaccion obtenida en la etapa a), que incluye un cierto numero de sales de aluminio, es hidrolizada con un acido clorhndrico acuoso.In step a) a Friedel Crafts reaction is used using the chlorobenzene itself as the solvent and aluminum chloride as the Lewis acid for the Friedel-Crafts reaction. Aluminum chloride is used in a molar ratio with respect to phthalic acid anhydride which is> 2: 1. The use of less aluminum chloride leads to incomplete conversion. Preferably, in step a), the reaction is carried out at the reflux temperature of the fluorobenzene, which is 75-80 ° C. When the reaction is carried out at a lower temperature, the reaction rate decreases. Preferably, the reaction mixture obtained in step a), which includes a certain number of aluminum salts, is hydrolyzed with an aqueous hydrochloric acid.
En la etapa b), la reaccion se realiza usando hidrogeno gaseoso, opcionalmente en la presencia de un catalizador de Pd/C y usando isopropanol (iPrOH) como el disolvente. El uso de metanol (MeOH) en vez de aquel conduce a una velocidad de reaccion disminuida. El uso de agua conduce a la formacion de impurezas. Preferentemente, en la etapa b), la reaccion se realiza a una temperatura situada por encima de 45 °C. Por debajo de 45 °C, la reaccion es demasiado lenta.In step b), the reaction is carried out using gaseous hydrogen, optionally in the presence of a Pd / C catalyst and using isopropanol (iPrOH) as the solvent. The use of methanol (MeOH) instead leads to a decreased reaction rate. The use of water leads to the formation of impurities. Preferably, in step b), the reaction is carried out at a temperature above 45 ° C. Below 45 ° C, the reaction is too slow.
En la etapa c), se usan 2,3 equivalentes de dihidro-bis (2-metoxi-etoxi) aluminato de sodio ("RedAl"). El uso de menos cantidad del agente reductor podna conducir a una conversion mas baja. Preferentemente, en la etapa c), se usa el tolueno como el disolvente. El tolueno es el disolvente en el que se disuelve el dihidro-bis (2-metoxetox) aluminato de sodio ("RedAl") comercial. Debido a la naturaleza reactiva de este agente reductor, no es posible usar unos disolventes proticos. Por lo demas, no es necesario aislar el producto obtenido en la etapa (c) despues de un tratamiento, puesto que la solucion en tolueno, que comprende el producto, se usa tal como estaIn step c), 2.3 equivalents of sodium dihydro-bis (2-methoxy-ethoxy) aluminate ("RedAl") are used. The use of less of the reducing agent could lead to a lower conversion. Preferably, in step c), toluene is used as the solvent. Toluene is the solvent in which commercial sodium dihydro-bis (2-methoxetox) aluminate ("RedAl") is dissolved. Due to the reactive nature of this reducing agent, it is not possible to use protic solvents. Moreover, it is not necessary to isolate the product obtained in step (c) after a treatment, since the toluene solution, which comprises the product, is used as is
En la etapa d) se usa acido un clorhfdrico acuoso como el agente de cloracion. En la etapa d), la reaccion se realiza a 90 °C. La velocidad de reaccion es mas baja a una temperatura mas baja. En la etapa d), la reaccion se realiza en un recipiente cerrado (se genera una acumulacion de la presion hasta 151,987 MPa (1,5 atmosferas)). En un recipiente abierto se desprende parcialmente el acido clorhndrico.In step d) an aqueous hydrochloric acid is used as the chlorinating agent. In step d), the reaction is carried out at 90 ° C. The reaction rate is lower at a lower temperature. In step d), the reaction is carried out in a closed vessel (a pressure accumulation is generated up to 151,987 MPa (1.5 atmospheres)). In an open container, the hydrochloric acid is partially released.
En la etapa e), el producto obtenido a partir de la etapa d) se hace reaccionar con CO en el seno de una mezcla de THF y H2O, preferiblemente en una relacion de 1:1, usando un sistema catalftico que contiene Pd. El agua es necesaria para llevar a cabo la hidrolisis del compuesto complejo con paladio intermedio. Su combinacion con THF proporciona la mas alta conversion. Como un sistema catalftico para esta etapa de la reaccion, se usa preferiblemente el acetato de sodio. Si se omite el acetato de sodio, apenas tiene lugar ninguna reaccion. Otros sistemas comprenden el carbonato de potasio o la trietilamina. En la etapa e), la reaccion se realiza usando la trifenilfosfina (Pt^P) como un ligando para el paladio. Se han ensayado otros ligandos, pero los resultados no son mejores. La Ph3P es el compuesto mas corriente y se usa de manera preferente. De manera preferente en la etapa e) la reaccion se realiza a una presion de 0,4 MPa (4 bares). A la presion atmosferica, la reaccion es muy lenta. DeIn step e), the product obtained from step d) is reacted with CO within a mixture of THF and H2O, preferably in a 1: 1 ratio, using a catalytic system containing Pd. Water is necessary to carry out the hydrolysis of the complex compound with intermediate palladium. Its combination with THF provides the highest conversion. As a catalytic system for this stage of the reaction, sodium acetate is preferably used. If sodium acetate is omitted, hardly any reaction takes place. Other systems include potassium carbonate or triethylamine. In step e), the reaction is performed using triphenylphosphine (Pt ^ P) as a ligand for palladium. Other ligands have been tested, but the results are not better. Ph3P is the most common compound and is preferably used. Preferably in step e) the reaction is carried out at a pressure of 0.4 MPa (4 bar). At atmospheric pressure, the reaction is very slow. From
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manera preferente, en la etapa e) la reaccion se realiza a una temperatura de 80 °C. A una temperatura mas baja, la reaccion es mas lenta.preferably, in step e) the reaction is carried out at a temperature of 80 ° C. At a lower temperature, the reaction is slower.
El procedimiento de acuerdo con el invento se explicara ahora usando los siguientes ejemplos.The process according to the invention will now be explained using the following examples.
Parte experimentalExperimental part
Todos los materiales se adquirieron de proveedores comerciales y se usaron sin ninguna purificacion ulterior. Las reacciones se realizaron bajo una atmosfera de hidrogeno, cuando fuese necesario. En el laboratorio se usaron solamente unos recipientes de vidrio, en la instalacion experimental se usan unos recipientes de acero y revestidos con vidrio. Para cada reaccion, se recoge una muestra de la mezcla de reaccion y se analiza por medio de una HPLC (cromatograffa de fase liquida alto rendimiento).All materials were purchased from commercial suppliers and used without further purification. The reactions were carried out under a hydrogen atmosphere, when necessary. Only glass containers were used in the laboratory, steel and glass-coated containers are used in the experimental installation. For each reaction, a sample of the reaction mixture is collected and analyzed by means of an HPLC (high performance liquid phase chromatography).
EjemploExample
Etapa a) Acido [2-(4-fluoro-benzoM)-benzoico (Compuesto IV)Stage a) [2- (4-Fluoro-benzoM) -benzoic acid (Compound IV)
1. Una solucion del bromuro de p-fluorobenceno- magnesio (solucion 1,2 M en THF, 1 eq.) se anade a una solucion 0,4 M de anhndrido de acido ftalico en THF, de manera tal que la temperatura permanece por debajo de 30 °C. Despues de 1 hora, la mitad del disolvente se separa por destilacion y la mezcla de reaccion se agita durante una noche a la temperatura ambiente. El precipitado obtenido se separa por filtracion y se recoge en agua (0,3 l/mol). Se anaden el tolueno (1 l/mol) y el HClcp de manera tal que la temperatura permanezca por debajo de 35 °C. Despues de haber agitado durante 1 hora, la capa organica se evapora (a 50 °C, en vado) y el material solido obtenido se seca a 50 °C bajo vado. Rendimiento activo: 69 %.1. A solution of p-fluorobenzene magnesium bromide (1.2 M solution in THF, 1 eq.) Is added to a 0.4 M solution of phthalic acid anhydride in THF, so that the temperature remains below 30 ° C. After 1 hour, half of the solvent is distilled off and the reaction mixture is stirred overnight at room temperature. The precipitate obtained is filtered off and collected in water (0.3 l / mol). Toluene (1 l / mol) and HClcp are added so that the temperature remains below 35 ° C. After stirring for 1 hour, the organic layer is evaporated (at 50 ° C, in vacuum) and the solid material obtained is dried at 50 ° C under vacuum. Active yield: 69%.
2. Alternativamente, se puede realizar una reaccion de Friedel-Crafts. En un matraz inertizado, que contiene antndrido ftalico, se anade fluorobenceno (1,8 l/mol), seguido por una adicion cuidadosa de cloruro de aluminio (2,1 eq.). La mezcla de reaccion se calienta hasta 75 °C (se observa un desprendimiento de HCl). Despues de 3 horas a 75 °C, se anade agua, (1 l/mol). La capa organica se separa y se anade acido clorhndrico concentrado (0,1 l/mol). El fluorobenceno se separa por destilacion y la mezcla se enfna a 10 °C. El precipitado se separa por filtracion, se lava con agua y se seca a 65-70 °C. Rendimiento activo: 85 %.2. Alternatively, a Friedel-Crafts reaction can be performed. In an inertized flask, containing phthalic antidrido, fluorobenzene (1.8 l / mol) is added, followed by a careful addition of aluminum chloride (2.1 eq.). The reaction mixture is heated to 75 ° C (HCl evolution is observed). After 3 hours at 75 ° C, water is added, (1 l / mol). The organic layer is separated and concentrated hydrochloric acid (0.1 l / mol) is added. The fluorobenzene is distilled off and the mixture is cooled to 10 ° C. The precipitate is filtered off, washed with water and dried at 65-70 ° C. Active yield: 85%.
N.B. El fluorobenceno se puede recuperar lavando con una solucion alcalina y desechando la capa acuosa.N.B. The fluorobenzene can be recovered by washing with an alkaline solution and discarding the aqueous layer.
Etapa b) Acido [2-(4-fluoro-bencil)-benzoico (Compuesto V)Stage b) [2- (4-Fluoro-benzyl) -benzoic acid (Compound V)
En un matraz de hidrogenacion se anadieron el acido 2-(4-fluoro-benzoM)-benzoico, el eter monometflico de propilen glicol (1 l/mol) y el Pd/C al 10 % humedo (15 g/mol). La hidrogenacion se realizo a 50 °C durante 18 horas. Se anadio tiofeno (0,3 kg/mol) y el catalizador se separo por filtracion. El material filtrado se calento a 80 °C y se anadio agua (1,12 l/mol) a esa temperatura. La mezcla se calento a reflujo, luego se enfrio a 25 °C y se agito a esa temperatura durante 1 hora. El precipitado se separo por filtracion, se lavo con agua (1 l/mol) y se seco a 50 °C durante 18 horas. Rendimiento activo: 83 %.In a hydrogenation flask were added 2- (4-fluoro-benzoM) -benzoic acid, monomethyl ether of propylene glycol (1 l / mol) and wet 10% Pd / C (15 g / mol). The hydrogenation was carried out at 50 ° C for 18 hours. Thiophene (0.3 kg / mol) was added and the catalyst was filtered off. The filtrate was heated to 80 ° C and water (1.12 l / mol) was added at that temperature. The mixture was heated to reflux, then cooled to 25 ° C and stirred at that temperature for 1 hour. The precipitate was filtered off, washed with water (1 l / mol) and dried at 50 ° C for 18 hours. Active yield: 83%.
Etapa c) [2-(4-Fluoro-bencil)-fenil-metanol (Compuesto VI)Stage c) [2- (4-Fluoro-benzyl) -phenyl-methanol (Compound VI)
En un matraz inertizado, que contiene el acido 2-(4-fluoro-bencil)-benzoico (1 eq.), se anade tolueno (0,8 l/mol) y el recipiente se enfna a 0-5 °C. Se anade gota a gota el dihidro-bis (2-metoxi-etoxi) aluminato de sodio ("RedAl"). (1 M en tolueno, 2,3 eq.) y la mezcla de reaccion se agita a 5 °C durante 16 horas. Se anade gota a gota la acetona (3 eq.) a 5 °C y la mezcla se agita durante 15 minutos. La temperatura se deja subir a 25 °C. Se anade una solucion de hidroxido de sodio (5 eq.) y la mezcla se agita energicamente durante 20 minutos. La capa organica se separa y se lava de nuevo con una solucion acuosa de caracter ligeramente acido. La capa organica se filtra sobre Dicalite y se usa ulteriormente en la siguiente etapa.In an inertized flask, containing 2- (4-fluoro-benzyl) -benzoic acid (1 eq.), Toluene (0.8 l / mol) is added and the vessel is cooled to 0-5 ° C. Sodium dihydro-bis (2-methoxy-ethoxy) aluminate ("RedAl") is added dropwise. (1 M in toluene, 2.3 eq.) And the reaction mixture is stirred at 5 ° C for 16 hours. Acetone (3 eq.) Is added dropwise at 5 ° C and the mixture is stirred for 15 minutes. The temperature is allowed to rise to 25 ° C. A solution of sodium hydroxide (5 eq.) Is added and the mixture is stirred vigorously for 20 minutes. The organic layer is separated and washed again with a slightly acidic aqueous solution. The organic layer is filtered over Dicalite and used later in the next stage.
Etapa d) [2-(4-Fluoro-bencil)-fenil-clorometano (Compuesto VII)Stage d) [2- (4-Fluoro-benzyl) -phenyl-chloromethane (Compound VII)
En un recipiente inertizado, que contiene una solucion de [2-(4-fluoro-bencil)-fenil-metanol en tolueno, se anade HClcp (5 eq.), el recipiente se cierra y la mezcla se agita a 90 °C (se desarrolla una presion de 0,154 MPa (1,54 bares)). Despues de 6 horas a 90 °C, la mezcla se enfna a 25 °C y el recipiente se abre. Las capas se separan, la capa organica se lava con agua y luego con una solucion ligeramente alcalina, y se usa ulteriormente en la siguiente etapa.In an inertized container, containing a solution of [2- (4-fluoro-benzyl) -phenyl-methanol in toluene, HClcp (5 eq.) Is added, the container is closed and the mixture is stirred at 90 ° C ( a pressure of 0.154 MPa (1.54 bar) is developed). After 6 hours at 90 ° C, the mixture is cooled to 25 ° C and the container is opened. The layers are separated, the organic layer is washed with water and then with a slightly alkaline solution, and is subsequently used in the next stage.
Etapa e) Acido [2-(4-fluoro-bencil)-fenil-acetico (Compuesto I)Stage e) [2- (4-Fluoro-benzyl) -phenyl-acetic acid (Compound I)
Se dispusieron el [2-(4-fluoro-bencil)-fenil]-clorometano (1 eq,), el THF (1 l/mol), agua (0,7 l/mol), el Pd(OAc)2 (1,3 % en moles), el dppp (2,6 % en moles) y el acetato de sodio dentro de un reactor inertizado. La mezcla de reaccion se dispone bajo una presion de CO de 0,4 MPa (4 bares) y se deja agitar a 80 °C durante 20 horas. La capa organica se separa y se evapora bajo presion. Se anade el tolueno (0,75 l/mol) al residuo y el acido carboxflico se extrae con una solucion 2 N de hidroxido de sodio (0,75 l/mol). Las partfculas de paladio de color negro se retiran por filtracion sobre Celite. La capa acuosa se dispone dentro de un matraz y se anade acido acetico (0,9 l/mol). La mezcla se calienta a 80 °C y luego se deja enfriar espontaneamente. La cristalizacion comienza a alrededor de 50 °C. Los cristales se separan por filtracion a la temperatura ambiente, se lavan con agua y se secan para formar el acido[2- (4-Fluoro-benzyl) -phenyl] -chloromethane (1 eq.), THF (1 l / mol), water (0.7 l / mol), Pd (OAc) 2 ( 1.3 mol%), dppp (2.6 mol%) and sodium acetate inside an inertized reactor. The reaction mixture is placed under a CO pressure of 0.4 MPa (4 bar) and allowed to stir at 80 ° C for 20 hours. The organic layer separates and evaporates under pressure. Toluene (0.75 l / mol) is added to the residue and the carboxylic acid is extracted with a 2 N solution of sodium hydroxide (0.75 l / mol). The black palladium particles are removed by filtration over Celite. The aqueous layer is placed inside a flask and acetic acid (0.9 l / mol) is added. The mixture is heated to 80 ° C and then allowed to cool spontaneously. Crystallization begins at around 50 ° C. The crystals are filtered off at room temperature, washed with water and dried to form the acid
[2-(4-fluoro-bencil)-fenil]-acetico (91 %) de color negro. El tratamiento con carbon organico de 5 g del acido [2-(4- fluoro-bencil)-fenil]-acetico de color negro en 25 ml de una mezcla de acido acetico y agua (7/3) permite el aislamiento de unos cristales puros de color blanco del acido [2-(4-fluoro-bencil)-fenil]-acetico. Esta etapa se puede realizar antes de la primera adicion de acido acetico.[2- (4-Fluoro-benzyl) -phenyl] -acetic acid (91%) black. The treatment with organic carbon of 5 g of the black [2- (4- fluoro-benzyl) -phenyl] -acetic acid in 25 ml of a mixture of acetic acid and water (7/3) allows the isolation of crystals pure white [2- (4-fluoro-benzyl) -phenyl] -acetic acid. This stage can be performed before the first addition of acetic acid.
5 Cada una de las etapas ha sido optimizada en el laboratorio y luego aumentada a escala satisfactoriamente en la instalacion experimental.5 Each of the stages has been optimized in the laboratory and then successfully scaled up in the experimental facility.
Claims (3)
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| Application Number | Priority Date | Filing Date | Title |
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| WOPCT/EP2004/051969 | 2004-08-31 | ||
| EP2004051969 | 2004-08-31 | ||
| PCT/EP2005/054202 WO2006024630A1 (en) | 2004-08-31 | 2005-08-26 | Process for the production of [2- (4-fluoro-benzyl) -phenyl] -acetic acid |
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| ES2562770T3 true ES2562770T3 (en) | 2016-03-08 |
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| ES05787232.7T Expired - Lifetime ES2562770T3 (en) | 2004-08-31 | 2005-08-26 | Process for the production of [2- (4-fluoro-benzyl) -phenyl] -acetic acid |
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| Country | Link |
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| US (1) | US7470809B2 (en) |
| JP (1) | JP2008511582A (en) |
| CN (1) | CN100591652C (en) |
| AU (1) | AU2005279211B2 (en) |
| CA (1) | CA2577305C (en) |
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| WO (1) | WO2006024630A1 (en) |
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| CN102746142A (en) * | 2012-06-27 | 2012-10-24 | 盛世泰科生物医药技术(苏州)有限公司 | Method for synthesis of 2-(2-(4-chlorphenyl)phenyl)acetic acid |
| CN102976929A (en) * | 2012-11-26 | 2013-03-20 | 盛世泰科生物医药技术(苏州)有限公司 | Method for synthesizing (4-chloro-2-phenoxy phenyl)-acetic acid |
| CN117486706B (en) * | 2024-01-02 | 2024-04-19 | 山东国邦药业有限公司 | A kind of synthetic method of 2,4,5-trifluorophenylacetic acid |
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| US6601146B2 (en) * | 1998-06-16 | 2003-07-29 | International Business Machines Corporation | Technique for efficiently transferring moderate amounts of data across address space boundary |
| DE10057262A1 (en) * | 2000-11-18 | 2002-05-23 | Clariant Gmbh | Process for the preparation of phenylacetic acid derivatives |
| CA2468040A1 (en) * | 2001-12-07 | 2003-06-12 | Janssen Pharmaceutica N.V. | Preparation of cis-fused 3,3a,8,12b-tetrahydro-2h-dibenzo[3,4:6,7]cyclohepta[1,2-b]furan derivatives |
| BR0214068A (en) * | 2001-12-07 | 2004-10-13 | Janssen Pharmaceutica Nv | Preparation of transfused 3,3a, 8,12b-tetrahydro-2h-dibenzo [3,4: 6,7] cyclohepta [1,2-b] furan derivatives |
| CN1690042A (en) * | 2004-04-30 | 2005-11-02 | 庄罗元 | Preparation method of 2-amino-4' -fluoro-benzophenone |
-
2005
- 2005-08-26 US US11/574,300 patent/US7470809B2/en not_active Expired - Lifetime
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| AU2005279211A1 (en) | 2006-03-09 |
| AU2005279211B2 (en) | 2011-07-28 |
| CA2577305C (en) | 2013-12-17 |
| US7470809B2 (en) | 2008-12-30 |
| WO2006024630A8 (en) | 2006-06-22 |
| WO2006024630A1 (en) | 2006-03-09 |
| CN101006039A (en) | 2007-07-25 |
| CN100591652C (en) | 2010-02-24 |
| JP2008511582A (en) | 2008-04-17 |
| CA2577305A1 (en) | 2006-03-09 |
| US20070213556A1 (en) | 2007-09-13 |
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